A. Spiess et al., pH gradients in immobilized amidases and their influence on rates and yields of beta-lactam hydrolysis, BIOTECH BIO, 62(3), 1999, pp. 267-277
The pH gradients developing within immobilized biocatalysts during hydrolys
is of penicillin G and glutaryl-7-aminocephalosporanic acid have been estim
ated both theoretically and experimentally. For the latter a fluorimetric m
ethod for the direct measurement of the average pH value within the carrier
during reaction has been developed using the pH-dependent fluorescence int
ensity of an enzyme-bound fluorophore determined with a fiber bundle. The t
heoretical calculations were based on a model for the hydrolysis with immob
ilized enzymes using a kinetic expression with five pH-dependent, measurabl
e kinetic and equilibrium constants. The transport reaction differential eq
uation which considers the laminar boundary layer has been solved numerical
ly for the key component. The calculated values agreed well with the experi
mental data. Under the typical reaction conditions of penicillin G hydrolys
is the average pH value in the carrier was 1 and 2.5 pH units below the bul
k pH (=8) with and without buffer, respectively. The corresponding changes
for the hydrolysis of glutaryl-7-aminocephalosporanic acid at bulk pH 8 in
the presence of buffer was 0.5. This demonstrates the existence of consider
able pH gradients in carriers during hydrolytic reactions, even in buffered
systems with negligible mass transfer resistance. The low pH value causes
suboptimal reaction rates, reduced equilibrium conversion, and reduced enzy
me stability. These pH gradients can be minimised by using buffers with pK
values approximately equal to the bulk pH used for the hydrolysis. The pred
iction quality of the model has been tested applying it to fixed bed reacto
r design. The reduction in rate and yield due to concentration and pH gradi
ents can be overcome with simple measures such as high initial pH value and
pH adjustments in segmented or recycling fixed bed reactors. Thus, enzymat
ic conversions with high yield and high operational effectiveness are achie
ved. (C) 1999 John Wiley & Sons, Inc.